Data for the LJ fluid properties: a pressure variation with density, and b viscosity variation with density. MD data points from pre-simulation (circles), fitted polynomial (solid lines) and NIST data (Linstrom and Mallard 2001) (dashed lines)

Data for the LJ fluid properties: a pressure variation with density, and b viscosity variation with density. MD data points from pre-simulation (circles), fitted polynomial (solid lines) and NIST data (Linstrom and Mallard 2001) (dashed lines)

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We present a procedure for using molecular dynamics (MD) simulations to provide essential fluid and interface properties for subsequent use in computational fluid dynamics (CFD) calculations of nanoscale fluid flows. The MD pre-simulations enable us to obtain an equation of state, constitutive relations, and boundary conditions for any given fluid/...

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... Bulk pressure as a function of bulk density Figure 2a shows MD pre-simulation measurements of pressure, obtained from the standard Irving and Kirkwood expression (1950), varying with the mass density. ...
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... to a second-order polynomial. This then serves as an equation of state within the enhanced CFD solver to connect the mass continuity equation to the momentum equation. In this case, the polynomial is p ¼ 0:001559q 2 À 3:387q þ 2020:6. For reference, data from the NIST database for argon (Linstrom and Mallard 2001) are also plotted in Fig. 2a and is in close agreement with our MD pre-simulation data. Clearly, in this particular case, properties for argon are well known, but we extract the equation of state from our MD pre- simulation for the purposes of demonstration. The equation of state (and the viscosity equation in the following subsection) could be obtained by ...
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... the relaxed and time-averaged velocity profile. The applied shear stress is measured using the Irving-Kirkwood equation and then compared with the strain rate using Eq. (1) to give a dynamic shear viscosity coefficient for L-J argon at a given bulk density. The vis- cosity coefficients measured from our MD pre-simulations of LJ argon are shown in Fig. 2b. A least-squares poly- nomial fit of 2nd order in density is also plotted: l ¼ 7:96 Â 10 À10 q 2 À 1:774 Â 10 À6 q þ 0:001106. This is then used in our enhanced CFD simulations to close the momentum equation. Again, for reference, data from the NIST database for liquid argon are also plotted in Fig. 2b. Note, due to the breakdown of ...
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... MD pre-simulations of LJ argon are shown in Fig. 2b. A least-squares poly- nomial fit of 2nd order in density is also plotted: l ¼ 7:96 Â 10 À10 q 2 À 1:774 Â 10 À6 q þ 0:001106. This is then used in our enhanced CFD simulations to close the momentum equation. Again, for reference, data from the NIST database for liquid argon are also plotted in Fig. 2b. Note, due to the breakdown of the continuum assumption and the existence of non-local stress, this state-dependent viscosity becomes only approximate when applied to a nano-confined ...
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... substantially affect the bulk density measured. The no-slip CFD model does not exhibit large pressure drops at the inlet and the outlet due to the much lower velocity in the tube (and therefore, there are lower accelerations at the inlet and outlet) than in the slip cases. Cross-sectional velocity profiles in the centre of the CNT are plotted in Fig. 12a. The mass flow rate in the full MD simulation is measured to be 4:3 Â 10 À14 kg/s, which is 23 % greater than that predicted by our enhanced CFD. That this is a significant improvement on conventional CFD model pre- dictions is indicated in Table ...
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... the $ 2 nm diameter of the (15,15) CNT and despite the molecular layering that actually occurs within the flow field, as evidenced in Fig. 12b, our enhanced CFD approach can be considered reasonably robust in predicting important averaged fluid properties to the correct order of magnitude. These CFD results are obtained with negligible cost in comparison with full MD ...

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